SK282374B6 - Production method of sugar syrup from raw materials containing sugar - Google Patents
Production method of sugar syrup from raw materials containing sugar Download PDFInfo
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- SK282374B6 SK282374B6 SK1643-99A SK164399A SK282374B6 SK 282374 B6 SK282374 B6 SK 282374B6 SK 164399 A SK164399 A SK 164399A SK 282374 B6 SK282374 B6 SK 282374B6
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- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B30/00—Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
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- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B50/00—Sugar products, e.g. powdered, lump or liquid sugar; Working-up of sugar
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- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B10/00—Production of sugar juices
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- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
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- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
- C13B20/14—Purification of sugar juices using ion-exchange materials
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- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
- C13B20/16—Purification of sugar juices by physical means, e.g. osmosis or filtration
- C13B20/165—Purification of sugar juices by physical means, e.g. osmosis or filtration using membranes, e.g. osmosis, ultrafiltration
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- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
- C13B20/18—Purification of sugar juices by electrical means
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- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Biochemistry (AREA)
- Engineering & Computer Science (AREA)
- Crystallography & Structural Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Food Science & Technology (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Jellies, Jams, And Syrups (AREA)
- Non-Alcoholic Beverages (AREA)
- Saccharide Compounds (AREA)
- Preparation Of Fruits And Vegetables (AREA)
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Abstract
Je opísaný spôsob výroby rafinovaného cukrového sirupu z poľnohospodárskych odpadov obsahujúcich cukor, ktorý obsahuje nasledujúce operácie: spracovanie okyslením za tepla brečky obsahujúcej cukor, uskutočnenie elektrolytického a ultrafiltračného spracovania tejto brečky; úpravy brečky v ionotmeničových stĺpcoch so sorbentom; jej kondenzovanie použitím reverznej osmózy; a odparenie brečky na koncentráciu zabezpečujúcu predĺženú životnosť. Brečka je priemyselne a bezpečne čistená s použitím ultrafiltrácie, reverznej osmózy a ionotmeničových membrán, počas procesu premeny odpadu. Produkt obsahujúci cukor, získaný uvedeným spôsobom, môže byť použitý v rôznych priemyselných odboroch ako je výroba cukroviniek, nealkoholického piva a v konzervárenstve, pri pečení chleba alebo pri kryštalizácii rafinovaného cukru.ŕA process for the production of refined sugar syrup from sugar-containing agricultural wastes is described, comprising the following operations: heat-treating the sugar-containing slurry, performing electrolytic and ultrafiltration processing of the slurry; slurry treatments in ion exchange columns with sorbent; its condensation using reverse osmosis; and evaporating the slurry to a concentration that provides extended life. The slurry is industrially and safely cleaned using ultrafiltration, reverse osmosis and ion exchange membranes, during the waste conversion process. The sugar-containing product obtained in this way can be used in various industries, such as the production of confectionery, non-alcoholic beer and in canning, in the baking of bread or in the crystallization of refined sugar.
Description
Oblasť technikyTechnical field
Vynález sa týka cukrovarníckeho priemyslu. Cukor obsahujúci výrobok, získaný použitím vynálezu je možné použiť v cukrárstve, pekárstve, konzervárenstve, pivovarníctve a pri výrobe nealkoholických nápojov.The invention relates to the sugar industry. The sugar-containing product obtained using the invention can be used in confectionery, bakery, canning, brewing and in the production of soft drinks.
Doterajší stav technikyBACKGROUND OF THE INVENTION
Je známe, že existuje spôsob získavania cukrového sirupu ako medziproduktu pri normálnej výrobe cukru (A. R. Sapronov, L.D. Bobrovnik „Sugar“, Moscow, „Light and food inustries, 1981). Spôsob obsahuje získanie šťavy, jej čistenie saturáciou, čerením a odparovaním. Nevýhody tohto spôsobu sú: vysoká spotreba energie pri odparovaní a nedostatočná kvalita sirupu, ktorá vyžaduje nákladný proces čistenia, aby sa získal biely kryštalický cukor z cukrového sirupu. Ďalej, obvyklý spôsob spracovania vyžaduje ďalšie pomocné prevádzky ako je úpravovňa vody, vápenka, tepláreň, sklad cukrovej repy, v jednom komplexe s výrobou cukru. Najpodobnejší tomuto spôsobu je spôsob získavania sirupu z materiálov obsahujúcich cukor, pozostávajúci z čistenia šťavy od nečistôt mechanickou filtráciou, ultrafiltráciou šťavy, iontomeničovým čistením, prechádzaním cez anionty a kationty, z koncentrácie roztoku reverznou osmózou a z odparovania, aby sa vytvoril sirup. (RU patent 2016637, C 13 F 1/00, 1994). Hlavnými nevýhodami tohto spôsobu sú: Nízka kapacita ultrafiltrácie upravená difúziou šťavy, ktorá je bohatá na vysokomolekulárne zlúčeniny a soľ. Následkom toho vznikajú požiadavky na častú regeneráciu membrán a regenerácia iontových zmesí špeciálnym roztokom je mimoriadne pomalá, dochádza k nedostatočnému odsoleniu, vzhľadom na premenu katióntov na formu Na+ pri regenerácii.It is known that there is a method of obtaining sugar syrup as an intermediate in normal sugar production (AR Sapronov, LD Bobrovnik "Sugar", Moscow, "Light and Food Inustries, 1981"). The method comprises obtaining the juice, purifying it by saturation, blackening and evaporation. The disadvantages of this method are: high evaporation energy consumption and poor syrup quality, which requires an expensive purification process to obtain white crystalline sugar from sugar syrup. Furthermore, the usual processing method requires additional auxiliary operations such as a water treatment plant, lime plant, heating plant, sugar beet store, in one complex with sugar production. Most similar to this method is a method of obtaining a syrup from sugar-containing materials, consisting of purifying juice from impurities by mechanical filtration, ultrafiltration of juice, ion exchange purification, passing through anions and cations, from solution concentration by reverse osmosis, and evaporating to form a syrup. (RU Patent 2016637, C13F 1/00, 1994). The main drawbacks of this method are: Low ultrafiltration capacity adjusted by the diffusion of juice, which is rich in high molecular weight compounds and salt. As a result, there is a requirement for frequent regeneration of membranes and regeneration of ionic mixtures with a special solution is extremely slow, with insufficient desalination due to the conversion of cations to the Na + form during regeneration.
Podstata vynálezuSUMMARY OF THE INVENTION
Problém je vyriešený vynálezom, ktorého podstatou je spôsob výroby cukrového sirupu rafinovanej čistoty z poľnohospodárskeho odpadu obsahujúceho cukor. Technický výsledok zaručuje rovnakú životnosť použitých zariadení, zdokonalenie kvality konečného produktu a vytvorenie ekologicky čistého procesu. Toto sa dosiahne navrhnutým spôsobom výroby cukrového sirupu zo suroviny, obsahujúcej cukor, ktorý pozostáva z rozrezania suroviny, získania šťavy, jej ultrafiltrácie, iontomeničovým čistením, koncentráciou reverznou osmózou a odparením, aby vznikol sirup; pred ultrafiltráciou sa pri tomto spôsobe šťava alebo rozrezaná surovina čistí okyslením, aby sa znížila hodnota pH, ohrieva sa, kým začnú proteíny koagulovať, potom sa odstráni filtráciou alebo odstredením, elektrolýza prebieha s použitím aktívnych elektród, ktoré dávajú pri rozpúšťaní polyvalentné ionty, ktoré spôsobujú koaguláciu koloidov s ďalším odstránením zrazenín; získaný produkt ultrafiltrácie pred iontomeničovým čistením je vystavený elektrodialýze na jeho demineralizáciu a potom roztok, obsahujúci cukor prechádza filtrom so sorbentom. Po elektrolýze šťavy musí byť v prípade nedostatočnej koagulácie vstrekovaná kyselina alebo soľ polyvalentného kovu na zrážanie koloidov s nasledovným oddelením zrazenín.The problem is solved by the invention, which is based on a process for producing refined purity sugar syrup from sugar-containing agricultural waste. The technical result ensures the same lifetime of the equipment used, the improvement of the end product quality and the creation of an environmentally clean process. This is achieved by the proposed method of producing sugar syrup from a sugar-containing raw material which comprises cutting the raw material, obtaining the juice, ultrafiltrating it, ion exchange purification, reverse osmosis concentration and evaporation to form a syrup; prior to ultrafiltration, the juice or chopped raw material is purified by acidification to lower the pH, heated until the proteins begin to coagulate, then removed by filtration or centrifugation, electrolysis is carried out using active electrodes which give polyvalent ions causing dissolution coagulation of colloids with further clot removal; the obtained ultrafiltration product prior to ion exchange purification is subjected to electrodialysis for its demineralization and then the sugar-containing solution is passed through a sorbent filter. After the electrolysis of the juice, in the case of insufficient coagulation, the acid or polyvalent metal salt must be injected to precipitate colloids, followed by separation of the precipitates.
Príklady uskutočnenia vynálezuDETAILED DESCRIPTION OF THE INVENTION
Cukor obsahujúci materiály musí byť, ak je to potrebné, prepraný. Potom sa rozrežú a v niektorých odpadoch musí byť uskutočnené okyslenie vstrekovaním látky, ktorá znižuje hodnotu pH, aby proteíny obsiahnuté v materiáli koagulovali. Šťava sa získava z rozrezaného materiálu odstreďovaním, lisovaním alebo difúziou alebo ich kombináciou. Šťava sa ohreje až začnú koagulovať v nej obsiahnuté proteíny a je okyslená (pokiaľ sa neokyslil už rozrezaný materiál) vstrekovaním látky, ktorá znižuje hodnotu pH prostredia, dokiaľ sa neobjaví suspendovaná zrazenina. Zrazenina sa odstraňuje filtráciou alebo odstredením šťavy. Takto vyčistená šťava sa vystaví elektrolýze v elektrolyzére s aktívnymi elektródami, ktoré dávajú pri rozpúšťaní polyvalentné ionty; tento proces pôsobí kým skolagujú koloidy obsiahnuté v šťave. V prípade nedostatočnej koagulácie elektrolyzovaný roztok musí byť upravovaný kyselinou alebo soľou polyvalentného kovu, pokiaľ sa koloidy nezrazia. Potom sa táto zrazenina oddelí filtráciou alebo odstredením a potom prebehne ultrafiltrácia. Potom ultrafiltrovaná šťava prechádza elektrodialyzérom, kde prebieha elekrodialýza na zníženie obsahu minerálnych látok, ktorá sa zlepší zmenou elektrickej vodivosti šťavy. Potom na dokončenie demineralizácie, šťava prebieha ionomeničovými filtrami a na odstránenie repnej chuti, prechádza filtrami so sorbentom. Potom sa uskutočňuje koncentrácia šťavy reverznými osmotickými membránami a odparovanie získaného sirupu, dokiaľ nie je obsah sušiny taký, aby bolo možné dlhodobé skladovanie bez kryštalizácie. Získaný cukor obsahujúci produkt, spĺňa požiadavku na index farby, čistotu, mikrobiologické vlastnosti a obsah toxických látok a pesticídov podľa ruského štandardu 22-94 na rafinovaný cukor. Táto kvalita, cukor obsahujúceho produktu, dovoľuje vypustiť čistenie uskutočnené počas výroby kryštalického cukru.Sugar containing materials must be washed if necessary. They are then cut and, in some wastes, acidification must be carried out by injecting a substance which lowers the pH to coagulate the proteins contained in the material. The juice is obtained from the cut material by centrifugation, pressing or diffusion or a combination thereof. The juice is heated until the proteins contained therein coagulate and is acidified (unless the already cut material has been acidified) by injecting a substance that lowers the pH of the environment until a suspended precipitate appears. The precipitate is removed by filtration or by centrifuging the juice. The juice thus purified is subjected to electrolysis in an electrolyzer with active electrodes which give polyvalent ions upon dissolution; this process works until the colloids contained in the juice collapse. In the case of insufficient coagulation, the electrolysed solution must be treated with an acid or polyvalent metal salt until the colloids precipitate. The precipitate is then collected by filtration or centrifugation and ultrafiltration is performed. Thereafter, the ultrafiltered juice passes through an electrodialyser, where electrodialysis takes place to reduce the mineral content, which is improved by changing the electrical conductivity of the juice. Then, to complete the demineralization, the juice is passed through ion exchange filters and to remove the beet taste, passed through the sorbent filters. The juice is then concentrated by reverse osmosis membranes and the obtained syrup is evaporated until the solids content is such that long-term storage without crystallization is possible. The obtained sugar containing the product meets the requirements for color index, purity, microbiological properties and the content of toxic substances and pesticides according to Russian standard 22-94 for refined sugar. This quality, the sugar-containing product, makes it possible to omit the purification carried out during the production of crystalline sugar.
Pri výhodnom uskutočnení vynálezu sa urobí difúzia repnej šťavy, ktorá má sacharózu 13,2 %, koeficient čistoty 82 %, obsah sušiny 16,1 %, vyrobené z dlho skladovanej repy, sa ohreje na 90 °C, okyslí sa kyselinou chlorovodíkovou na hodnotu pH 4,5; objavujúce sa zrazené proteíny sa filtrujú. Takto získaná zrazenina je proteínpolosacharidový koncentrát, ktorý neobsahuje žiadne nebezpečné látky a môže sa pridávať do lisovanej repy na kŕmenie dobytka. Filtrovaná šťava, ktorá má koeficient čistoty 89 % je spracovaná elektrolýzou v elektrolyzéri s hliníkovými elektródami s potenciálom medzi elektródami 2,5 V, hustotou prúdu 5 A/cm2, pokiaľ nenastane zrážanie hydroxidu hlinitého. Do roztoku spracovávaného elektrolýzou sa musí vstrekovať zmes 30 % roztoku síranu hlinitého až dôjde k oddeleniu fáz; potom sa roztok filtruje, aby sa odstránili zrazeniny. Filtrovaná látka, spracovaná elektrolýzou má koeficient čistoty 91,6 %, neobsahuje farebné nečistoty, obsahuje malé množstvo vysokomolekulárnych zlúčenín a má hodnotu pH 6,95. Látka spracovaná elektrolýzou je vystavená ultrafiltrácii na odstránenie zbytkových vysokomolekulárnych zlúčenín s tlakom 0,3 Pa na membránach, vyrobených z aromatického polyamidu. Ultrafiltrovaná látka sa spracováva v elekrodialyzére iontomeničovými membránami MK-40 a MA-40 a meria sa jej elektrická vodivosť. Po dosiahnutí zníženia o desaťnásobok, sa proces zastaví. Potom sa uskutoční postupná demineralizácia kationitom IMAC HP 1110, anionitom IMAC HP 661 a katinitom IMAC HP 336 a potom sa čistí aktívnym uhlím. Získaný roztok má obsah sušiny 13 %, koeficient čistoty 99,9 % a nulový index farby. Potom sa získaný roztok koncentruje reverznou osmózou na membránach vyrobených z a2 romatického polyamidu, dokiaľ nie je obsah sacharózy 35 % a potom sa koncentrát odparí až na obsah sacharózy 99,9 %, čo znamená, že spĺňa podmienky ruského štandardu 22-94 na rafinovaný cukor.In a preferred embodiment of the invention, the beet juice having a sucrose 13.2%, a purity coefficient of 82%, a dry matter content of 16.1% made from long-stored beet, is heated to 90 ° C, acidified with hydrochloric acid to pH 4.5; emerging precipitated proteins are filtered. The precipitate thus obtained is a protein polosaccharide concentrate which does not contain any hazardous substances and can be added to pressed beet for cattle feeding. The filtered juice having a purity coefficient of 89% is processed by electrolysis in an electrolyzer with aluminum electrodes with a potential between the electrodes of 2.5 V, a current density of 5 A / cm 2 until precipitation of aluminum hydroxide occurs. A mixture of 30% aluminum sulphate solution must be injected into the electrolysis solution until phase separation occurs; then the solution is filtered to remove precipitates. The filtered electrolysis material has a purity coefficient of 91.6%, does not contain color impurities, contains a small amount of high molecular weight compounds and has a pH of 6.95. The electrolyzed substance is subjected to ultrafiltration to remove residual high molecular weight compounds at 0.3 Pa on membranes made of aromatic polyamide. The ultrafiltered material is processed in an electrodialyser by MK-40 and MA-40 ion-exchange membranes and its electrical conductivity is measured. When the reduction is ten times, the process stops. Subsequently, sequential demineralization is performed with the cationite IMAC HP 1110, the anionite IMAC HP 661 and the catinite IMAC HP 336, and then purified with activated carbon. The obtained solution has a dry matter content of 13%, a purity coefficient of 99.9% and a zero color index. Then the solution obtained is concentrated by reverse osmosis on membranes made of α2 romatic polyamide until the sucrose content is 35% and then the concentrate is evaporated to a sucrose content of 99.9%, which means that it complies with the Russian standard 22-94 for refined sugar .
Priemyselná využiteľnosťIndustrial usability
Na základe navrhnutého spôsobu výroby cukrového sirupu môže byť vytvorená rafinéria nového typu, v ktorej sa spôsob výroby cukrového sirupu z akéhokoľvek materiálu obsahujúceho cukor stáva výnosným a spĺňa súčasné ekologické požiadavky. Prevádzka takýchto rafinérií zaručuje, počas čistenia, rovnomerné rozdelenie pracovného zaťaženia všetkých operácií technologického procesu a tiež zaručuje rovnakú životnosť všetkých zariadení, zlepšia sa pracovné podmienky pri ultrafiltrácii jednotiek na reverznú osmózu a pri odparovaní. Pri výrobe cukru z cukrového sirupu, získaného podľa navrhnutého spôsobu, nie je potrebné čistiť sirup počas výroby, pretože sirup bude mať čistotu rafinovaného cukru.On the basis of the proposed method of producing sugar syrup, a refinery of a new type can be created in which the method of producing sugar syrup from any sugar-containing material becomes profitable and meets current environmental requirements. The operation of such refineries ensures, during cleaning, a uniform distribution of the workload of all process operations and also guarantees an equal lifetime of all equipment, the working conditions for ultrafiltration of reverse osmosis units and evaporation are improved. In the production of sugar from the sugar syrup obtained according to the proposed method, it is not necessary to purify the syrup during manufacture since the syrup will have the purity of the refined sugar.
Claims (2)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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RU97109286/13A RU2114177C1 (en) | 1997-06-02 | 1997-06-02 | Method of production of sugar syrup from sugar-containing raw |
PCT/RU1998/000147 WO1998055658A2 (en) | 1997-06-02 | 1998-05-18 | Method for producing sugar syrup from sugar-containing raw materials |
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SK164399A3 SK164399A3 (en) | 2000-09-12 |
SK282374B6 true SK282374B6 (en) | 2002-01-07 |
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US (1) | US6372049B1 (en) |
EP (1) | EP0994194A4 (en) |
JP (1) | JP2002502259A (en) |
KR (1) | KR20010013268A (en) |
CN (1) | CN1089114C (en) |
AU (1) | AU726865B2 (en) |
BG (1) | BG104047A (en) |
BR (1) | BR9809901A (en) |
CA (1) | CA2295659A1 (en) |
CU (1) | CU22761A3 (en) |
EA (1) | EA002226B1 (en) |
EE (1) | EE03835B1 (en) |
HU (1) | HUP0003016A3 (en) |
ID (1) | ID23017A (en) |
LV (1) | LV12434B (en) |
NZ (1) | NZ502049A (en) |
PL (1) | PL337462A1 (en) |
RO (1) | RO120851B1 (en) |
RU (1) | RU2114177C1 (en) |
SK (1) | SK282374B6 (en) |
TR (1) | TR199903021T2 (en) |
WO (1) | WO1998055658A2 (en) |
YU (1) | YU62599A (en) |
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ECSP024245A (en) * | 2002-04-08 | 2002-06-26 | Illingworth Fernando Martinez | PROCESS AND TWO APPLIANCES FOR OBTAINING SYRUP OF VARIOUS SUGARS FROM AN ENZYMATIC EXTRACTION OF FRUIT PULP AND USING RESINS, ACCOMPANIED BY A NEW MIXED EVAPORATION AND PURIFICATION SYSTEM |
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RU2366718C2 (en) * | 2004-03-19 | 2009-09-10 | Органо Корпорэйшн | Method for purifying of sugar solutions |
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CN104323268A (en) | 2006-09-19 | 2015-02-04 | 视界科技有限公司 | Extracts derived from sugar cane and a process for their manufacture |
WO2012106761A1 (en) | 2011-02-08 | 2012-08-16 | Horizon Science Pty Ltd | Sugar extracts |
WO2014032100A1 (en) | 2012-08-28 | 2014-03-06 | Phytolin Pty Ltd | Extraction method |
US9622505B2 (en) | 2013-03-14 | 2017-04-18 | H2O Innovation Inc. | System and method to produce maple syrup |
AU2014306366B9 (en) | 2013-08-16 | 2020-03-26 | Poly Gain Pte Ltd | Sugar cane derived extracts and methods of treatment |
MX2013013972A (en) * | 2013-11-28 | 2015-05-28 | Héctor Alejandro Álvarez De La Cadena Sillas | Process for obtaining a sugar cane flavoring agent from concentrates of sugar cane or intermediate syrups and molasses derived from the extraction of sugar in sugar mills, as a high performance sweetening additive and resulting product. |
CN103725804A (en) * | 2013-12-20 | 2014-04-16 | 广西科技大学 | Method of improving apparent purity of sugar product |
CN103725803A (en) * | 2013-12-20 | 2014-04-16 | 广西科技大学 | Electrolytic clarification technology of ultrasonic enhanced liquid glucose |
WO2017042601A1 (en) * | 2015-09-11 | 2017-03-16 | Mathur Pradeep | A process for sugar extraction from sugar juices by removing impurities from raw sugar juices |
CN110342656A (en) * | 2018-04-02 | 2019-10-18 | 无锡甜丰食品有限公司 | A kind of condensation water treatment technology for syrup technique |
CN108676926B (en) * | 2018-06-01 | 2022-04-22 | 广西科技师范学院 | Production method of white granulated sugar |
CN111620958A (en) | 2020-04-25 | 2020-09-04 | 浙江工业大学 | Extraction and purification method of dendrobium officinale polysaccharide |
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SU86156A1 (en) * | 1949-10-13 | 1949-11-30 | Г.С. Бенин | The method of cleaning diffusion juice |
US3563799A (en) * | 1967-10-02 | 1971-02-16 | Industrial Filter Pump Mfg Co | Purified liquid sugar concentrate and method of manufacturing same |
GB1350261A (en) * | 1970-10-16 | 1974-04-18 | Hitachi Shipbuilding Eng Co | Sugar refining process |
US3799806A (en) * | 1972-04-20 | 1974-03-26 | Danske Sukkerfab | Process for the purification and clarification of sugar juices,involving ultrafiltration |
SU482496A1 (en) * | 1972-07-24 | 1975-08-30 | Киевский Технологический Институт Пищевой Промышленности | The method of purification of sugar-containing solution |
SU631535A1 (en) * | 1977-06-01 | 1978-11-05 | Всесоюзный научно-исследовательский институт сахарной промышленности | Method of purifying sugar-containing solution |
SE441932B (en) * | 1981-01-14 | 1985-11-18 | Danske Sukkerfab | PROCEDURE FOR PURIFICATION OF SUGAR SOFT PREPARED BY EXTRACTION OF SUGAR BEETS |
FR2570716B2 (en) * | 1982-03-05 | 1987-01-09 | Valorisation Agrobiologique | IMPROVED PROCESS FOR THE PHYSICO-CHEMICAL TREATMENT OF PLANTS, PARTICULARLY CARBOHYDRATE PLANTS |
AU555410B2 (en) * | 1982-10-15 | 1986-09-25 | Asahi Kasei Kogyo Kabushiki Kaisha | Removing salt impurities from sugar syrup or molasses |
DE3407364A1 (en) * | 1984-02-29 | 1985-08-29 | Pfeifer & Langen, 5000 Köln | NATURAL WHOLE CANE SUGAR AND METHOD FOR THE PRODUCTION THEREOF |
JPH0280000A (en) * | 1988-09-19 | 1990-03-20 | Hokuren Federation Of Agricult Coop:The | Production of sugar from beet sugar concentrate |
RU2016637C1 (en) * | 1992-06-25 | 1994-07-30 | Салдадзе Григорий Кириллович | Method of producing granulated sugar from sugar juices |
US5468300A (en) * | 1994-04-07 | 1995-11-21 | International Food Processing Incorporated | Process for producing refined sugar directly from sugarcane |
RU2114177C1 (en) | 1997-06-02 | 1998-06-27 | Товарищество с ограниченной ответственностью Центр содействия развитию новых технологий "Кантэк" | Method of production of sugar syrup from sugar-containing raw |
-
1997
- 1997-06-02 RU RU97109286/13A patent/RU2114177C1/en not_active IP Right Cessation
-
1998
- 1998-05-18 JP JP50220299A patent/JP2002502259A/en active Pending
- 1998-05-18 EE EEP199900552A patent/EE03835B1/en not_active IP Right Cessation
- 1998-05-18 EA EA199901036A patent/EA002226B1/en not_active IP Right Cessation
- 1998-05-18 NZ NZ502049A patent/NZ502049A/en unknown
- 1998-05-18 KR KR19997011260A patent/KR20010013268A/en not_active Application Discontinuation
- 1998-05-18 AU AU79442/98A patent/AU726865B2/en not_active Ceased
- 1998-05-18 HU HU0003016A patent/HUP0003016A3/en unknown
- 1998-05-18 BR BR9809901-9A patent/BR9809901A/en not_active IP Right Cessation
- 1998-05-18 YU YU62599A patent/YU62599A/en unknown
- 1998-05-18 CA CA002295659A patent/CA2295659A1/en not_active Abandoned
- 1998-05-18 TR TR1999/03021T patent/TR199903021T2/en unknown
- 1998-05-18 EP EP98929943A patent/EP0994194A4/en not_active Withdrawn
- 1998-05-18 SK SK1643-99A patent/SK282374B6/en unknown
- 1998-05-18 CN CN98807423A patent/CN1089114C/en not_active Expired - Fee Related
- 1998-05-18 RO RO99-01267A patent/RO120851B1/en unknown
- 1998-05-18 US US09/424,914 patent/US6372049B1/en not_active Expired - Fee Related
- 1998-05-18 WO PCT/RU1998/000147 patent/WO1998055658A2/en not_active Application Discontinuation
- 1998-05-18 PL PL98337462A patent/PL337462A1/en unknown
- 1998-05-18 ID IDW991502A patent/ID23017A/en unknown
-
1999
- 1999-12-01 LV LVP-99-171A patent/LV12434B/en unknown
- 1999-12-02 CU CU1999213A patent/CU22761A3/en unknown
- 1999-12-23 BG BG104047A patent/BG104047A/en unknown
Also Published As
Publication number | Publication date |
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SK164399A3 (en) | 2000-09-12 |
AU7944298A (en) | 1998-12-21 |
LV12434A (en) | 2000-02-20 |
ID23017A (en) | 1999-12-30 |
US6372049B1 (en) | 2002-04-16 |
JP2002502259A (en) | 2002-01-22 |
EA002226B1 (en) | 2002-02-28 |
BG104047A (en) | 2000-07-31 |
CN1089114C (en) | 2002-08-14 |
CN1273610A (en) | 2000-11-15 |
EP0994194A2 (en) | 2000-04-19 |
EE03835B1 (en) | 2002-08-15 |
KR20010013268A (en) | 2001-02-26 |
BR9809901A (en) | 2000-10-17 |
CA2295659A1 (en) | 1998-12-10 |
RO120851B1 (en) | 2006-08-30 |
AU726865B2 (en) | 2000-11-23 |
HUP0003016A3 (en) | 2001-02-28 |
EP0994194A4 (en) | 2000-05-31 |
WO1998055658A2 (en) | 1998-12-10 |
RU2114177C1 (en) | 1998-06-27 |
HUP0003016A2 (en) | 2001-01-29 |
EE9900552A (en) | 2000-06-15 |
YU62599A (en) | 2001-09-28 |
NZ502049A (en) | 2000-10-27 |
TR199903021T2 (en) | 2000-06-21 |
LV12434B (en) | 2000-05-20 |
CU22761A3 (en) | 2002-07-24 |
EA199901036A1 (en) | 2000-06-26 |
WO1998055658A3 (en) | 1999-03-04 |
PL337462A1 (en) | 2000-08-14 |
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